典型污水處理系統(tǒng)

1、謝謝！謝謝！結(jié)束結(jié)束點(diǎn)擊此處打開錄象返回ssQvaS1000返回返回返回返回返回返回返回返回返回g2vh20.40.9QB1.25Bh0)m(B8 . 9/)Q5 . 1 (h322k)m(gB/Q73. 1h3220返回n處理構(gòu)筑物之間連接管渠的設(shè)計(jì)n配水設(shè)備：要求均勻配水n計(jì)量設(shè)備返回處理構(gòu)筑物之間連接管渠的設(shè)計(jì)處理構(gòu)筑物之間連接管渠的設(shè)計(jì)返回配水設(shè)備配水設(shè)備返回返回返回返回n實(shí)例平面布置n實(shí)例高程布置返回實(shí)例平面布置實(shí)例平面布置返回返回實(shí)例高程布置實(shí)例高程布置返回構(gòu)筑物名稱水頭損失(cm)構(gòu)筑物名稱水頭損失(cm)格柵沉砂池沉淀池：平流豎流輻流雙層沉淀池曝氣池：污水潛流入池污水跌水入池1

2、02510252040405050601020255050150生物濾池(工作高度為2m時(shí))：1) 裝有旋轉(zhuǎn)式布水器2) 裝有固定噴灑布水器混合流或接觸池污泥干化場(chǎng)2702804504751030200350注：本表僅作為初步設(shè)計(jì)階段水頭損失的估算 設(shè)計(jì)點(diǎn)編號(hào)管渠名稱設(shè)計(jì)流量(L/s)管渠設(shè)計(jì)參數(shù)尺寸D(mm)或BH(m)h/D水深h(m)i流速v(m/s)長(zhǎng)度l(m)123456789EEF3F3F3F3DDF2F2CCF1F1F1F1出廠管入灌溉渠出廠管出廠管沉淀池出水總渠沉淀池集水槽沉淀池入流管計(jì)量堰曝氣池出水總渠曝氣池集水槽計(jì)量堰曝氣池配水渠往曝氣池配水渠沉淀池出水總渠沉淀池集水槽沉淀

3、池入流管計(jì)量堰沉淀池配水渠60060030015075/2150150600150300300300150150/2150150150100010006000.61.00.300.534500.841.00.60.550.840.856000.61.00.350.534500.81.50.80.80.750.80.80.450.350.250.380.640.420.260.620.540.350.250.440.480.460.0010.00350.00280.00240.00281.011.370.941.070.94390100282810482752811356.3055.5255.3

4、7 55.2555.20 55.10 54.6554.33 54.6353.76 53.6653.4453.2252.6450.8452.3852.1651.7551.4451.7450.9450.8450.4950.4450.2050.0549.25點(diǎn)8點(diǎn)7點(diǎn)6點(diǎn)5點(diǎn)4（灌溉渠）二次沉淀池43.74F3曝氣池點(diǎn)3點(diǎn)246.63初次沉淀池F1曝氣沉沙池格柵點(diǎn)153.3050.00圖 24- B市污水處理廠污水處理流程高程布置圖返回污泥處理高程設(shè)計(jì)-185. 117. 1)(49. 2HfCvDLh 污泥處理高程設(shè)計(jì)-2mhf2 . 1)715 . 1)(3 . 0150(49. 285. 11

5、7. 1 mhf20. 1)325 . 1)(2 . 070(49. 217. 1 m8 . 75 . 12 . 11 . 00 . 20 . 3 返回返回返回返回返回返回點(diǎn)擊此處觀看電滲析裝置工作過程點(diǎn)擊此處觀看液氯消毒工作過程點(diǎn)擊此處觀看臭氧消毒工作過程及臭氧與污水的混合反應(yīng)器返回H3)PO)(OH(CaHPO3OH4Ca5345242羥基磷灰石點(diǎn)擊此處觀看氨氣脫除塔工作過程返回返回返回返回返回) 11081. 9(1000)(40PCSAQCQsc返回返回返回返回污泥種類進(jìn)泥含水率（%）聚合物用量污泥干重（%）產(chǎn)泥能力kg干污泥/（mh）泥餅含水率（%）生污泥初次污泥90950.090.22504006575初次污泥+活性污泥9296.50.